WO2002043173A1 - Electrochemical polymer electrolyte membrane cell stacks - Google Patents
Electrochemical polymer electrolyte membrane cell stacks Download PDFInfo
- Publication number
- WO2002043173A1 WO2002043173A1 PCT/US2001/044880 US0144880W WO0243173A1 WO 2002043173 A1 WO2002043173 A1 WO 2002043173A1 US 0144880 W US0144880 W US 0144880W WO 0243173 A1 WO0243173 A1 WO 0243173A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- manifold
- flow field
- fuel cell
- electrode assembly
- membrane electrode
- Prior art date
Links
- 239000012528 membrane Substances 0.000 title claims abstract description 58
- 239000005518 polymer electrolyte Substances 0.000 title abstract description 5
- 239000000446 fuel Substances 0.000 claims abstract description 267
- 239000000376 reactant Substances 0.000 claims abstract description 70
- 229920005989 resin Polymers 0.000 claims abstract description 60
- 239000011347 resin Substances 0.000 claims abstract description 60
- 239000000565 sealant Substances 0.000 claims abstract description 48
- 239000007800 oxidant agent Substances 0.000 claims abstract description 45
- 239000002826 coolant Substances 0.000 claims abstract description 42
- 230000001590 oxidative effect Effects 0.000 claims abstract description 42
- 238000009826 distribution Methods 0.000 claims abstract description 21
- 230000002093 peripheral effect Effects 0.000 claims abstract description 20
- 230000015572 biosynthetic process Effects 0.000 claims description 36
- 230000006835 compression Effects 0.000 claims description 30
- 238000007906 compression Methods 0.000 claims description 30
- 238000000034 method Methods 0.000 claims description 28
- 238000004519 manufacturing process Methods 0.000 claims description 25
- 238000003860 storage Methods 0.000 claims description 11
- 239000000463 material Substances 0.000 claims description 9
- 229920001187 thermosetting polymer Polymers 0.000 claims description 9
- 229920001169 thermoplastic Polymers 0.000 claims description 6
- 239000004416 thermosoftening plastic Substances 0.000 claims description 6
- 239000002131 composite material Substances 0.000 claims description 4
- 238000005304 joining Methods 0.000 claims description 4
- 229920000642 polymer Polymers 0.000 claims description 4
- 239000012815 thermoplastic material Substances 0.000 claims description 4
- 239000003365 glass fiber Substances 0.000 claims description 3
- 229920001296 polysiloxane Polymers 0.000 claims description 3
- 230000000284 resting effect Effects 0.000 claims description 2
- 229910001092 metal group alloy Inorganic materials 0.000 claims 1
- 210000004027 cell Anatomy 0.000 description 198
- 102100025532 Male-enhanced antigen 1 Human genes 0.000 description 74
- 238000013461 design Methods 0.000 description 26
- 102100034256 Mucin-1 Human genes 0.000 description 19
- 238000002047 photoemission electron microscopy Methods 0.000 description 19
- 229920001483 poly(ethyl methacrylate) polymer Polymers 0.000 description 19
- 125000006850 spacer group Chemical group 0.000 description 16
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 12
- -1 polypropylene Polymers 0.000 description 11
- 238000007789 sealing Methods 0.000 description 11
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 9
- 239000007789 gas Substances 0.000 description 9
- 230000008569 process Effects 0.000 description 9
- 229910052799 carbon Inorganic materials 0.000 description 7
- 239000003054 catalyst Substances 0.000 description 7
- 238000005538 encapsulation Methods 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 6
- 239000004743 Polypropylene Substances 0.000 description 5
- 230000000712 assembly Effects 0.000 description 5
- 238000000429 assembly Methods 0.000 description 5
- 238000001816 cooling Methods 0.000 description 5
- 229920001971 elastomer Polymers 0.000 description 5
- 239000000806 elastomer Substances 0.000 description 5
- 229920001155 polypropylene Polymers 0.000 description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 4
- 239000003570 air Substances 0.000 description 4
- 210000003850 cellular structure Anatomy 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000003638 chemical reducing agent Substances 0.000 description 4
- 230000007797 corrosion Effects 0.000 description 4
- 238000005260 corrosion Methods 0.000 description 4
- 238000009792 diffusion process Methods 0.000 description 4
- 229910002804 graphite Inorganic materials 0.000 description 4
- 239000010439 graphite Substances 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 238000001721 transfer moulding Methods 0.000 description 4
- 239000000853 adhesive Substances 0.000 description 3
- 230000001070 adhesive effect Effects 0.000 description 3
- 239000000956 alloy Substances 0.000 description 3
- 229910045601 alloy Inorganic materials 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 239000006227 byproduct Substances 0.000 description 3
- 230000001419 dependent effect Effects 0.000 description 3
- 239000013536 elastomeric material Substances 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 230000007246 mechanism Effects 0.000 description 3
- 238000005065 mining Methods 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 229910052697 platinum Inorganic materials 0.000 description 3
- 229920000647 polyepoxide Polymers 0.000 description 3
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 3
- 239000004810 polytetrafluoroethylene Substances 0.000 description 3
- 239000004814 polyurethane Substances 0.000 description 3
- 229920003319 Araldite® Polymers 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- HEVGGTGPGPKZHF-UHFFFAOYSA-N Epilaurene Natural products CC1C(=C)CCC1(C)C1=CC=C(C)C=C1 HEVGGTGPGPKZHF-UHFFFAOYSA-N 0.000 description 2
- 239000004593 Epoxy Substances 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 125000003700 epoxy group Chemical group 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000007770 graphite material Substances 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229920002492 poly(sulfone) Polymers 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010936 titanium Substances 0.000 description 2
- 229910052719 titanium Inorganic materials 0.000 description 2
- 150000003673 urethanes Chemical class 0.000 description 2
- 229920001567 vinyl ester resin Polymers 0.000 description 2
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 2
- 229920003249 vinylidene fluoride hexafluoropropylene elastomer Polymers 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229920003934 Aciplex® Polymers 0.000 description 1
- 229910052582 BN Inorganic materials 0.000 description 1
- PZNSFCLAULLKQX-UHFFFAOYSA-N Boron nitride Chemical compound N#B PZNSFCLAULLKQX-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- 229920003935 Flemion® Polymers 0.000 description 1
- 229920000034 Plastomer Polymers 0.000 description 1
- 239000004721 Polyphenylene oxide Substances 0.000 description 1
- 239000004734 Polyphenylene sulfide Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 239000004433 Thermoplastic polyurethane Substances 0.000 description 1
- 239000003011 anion exchange membrane Substances 0.000 description 1
- 239000004760 aramid Substances 0.000 description 1
- 229920006231 aramid fiber Polymers 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 229920001940 conductive polymer Polymers 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 229920003247 engineering thermoplastic Polymers 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 230000009969 flowable effect Effects 0.000 description 1
- 229920002313 fluoropolymer Polymers 0.000 description 1
- 239000004811 fluoropolymer Substances 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229920003223 poly(pyromellitimide-1,4-diphenyl ether) Polymers 0.000 description 1
- 229920006393 polyether sulfone Polymers 0.000 description 1
- 229920001955 polyphenylene ether Polymers 0.000 description 1
- 229920006380 polyphenylene oxide Polymers 0.000 description 1
- 229920000069 polyphenylene sulfide Polymers 0.000 description 1
- 229920012287 polyphenylene sulfone Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229920003031 santoprene Polymers 0.000 description 1
- 239000003566 sealing material Substances 0.000 description 1
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 1
- 229910010271 silicon carbide Inorganic materials 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 150000003460 sulfonic acids Chemical class 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 229920002397 thermoplastic olefin Polymers 0.000 description 1
- 229920002803 thermoplastic polyurethane Polymers 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0271—Sealing or supporting means around electrodes, matrices or membranes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0258—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0267—Collectors; Separators, e.g. bipolar separators; Interconnectors having heating or cooling means, e.g. heaters or coolant flow channels
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0271—Sealing or supporting means around electrodes, matrices or membranes
- H01M8/028—Sealing means characterised by their material
- H01M8/0284—Organic resins; Organic polymers
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0271—Sealing or supporting means around electrodes, matrices or membranes
- H01M8/0286—Processes for forming seals
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1007—Fuel cells with solid electrolytes with both reactants being gaseous or vaporised
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/241—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/241—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
- H01M8/242—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes comprising framed electrodes or intermediary frame-like gaskets
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/2465—Details of groupings of fuel cells
- H01M8/247—Arrangements for tightening a stack, for accommodation of a stack in a tank or for assembling different tanks
- H01M8/2475—Enclosures, casings or containers of fuel cell stacks
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/2465—Details of groupings of fuel cells
- H01M8/247—Arrangements for tightening a stack, for accommodation of a stack in a tank or for assembling different tanks
- H01M8/248—Means for compression of the fuel cell stacks
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/2465—Details of groupings of fuel cells
- H01M8/2483—Details of groupings of fuel cells characterised by internal manifolds
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/249—Grouping of fuel cells, e.g. stacking of fuel cells comprising two or more groupings of fuel cells, e.g. modular assemblies
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Definitions
- This invention relates to electrochemical polymer electrolyte membrane (“PEM”) cells and stacks thereof, and more particularly, to PEM fuel cell stacks.
- PEM electrochemical polymer electrolyte membrane
- the present invention also describes novel processes for producing these PEM fuel cell stacks.
- Electrochemical PEM cells and particularly, PEM fuel cells are well known.
- PEM fuel cells convert chemical energy to electrical power with virtually no environmental emissions and differ from a battery in that energy is not stored, but derived from supplied fuel. Therefore, a fuel cell is not tied to a charge/discharge cycle and can maintain a specific power output as long as fuel is continuously supplied.
- the large investments into fuel cell research and commercialization indicate the technology has considerable potential in the marketplace.
- the high cost of fuel cells when compared to conventional power generation technology has deterred their potentially widespread use. Costs of fabricating and assembling fuel cells can be significant, due to the materials and labor involved, and as much as 85% of a fuel cell's price can be attributed to manufacturing costs.
- a single cell PEM fuel cell consists of an anode and a cathode compartment separated by a thin, ionically conducting membrane. This catalyzed membrane, with or without gas diffusion layers, is often referred to as a membrane electrode assembly ("MEA").
- MEA membrane electrode assembly
- Energy conversion begins when the reactants, reductants and oxidants, are supplied to the anode and cathode compartments, respectively, of the PEM fuel cell.
- Oxidants include pure oxygen, oxygen containing gases, such as air, and halogens, such as chlorine.
- Reductants, also referred to herein as fuel include hydrogen, natural gas, methane, ethane, propane, butane, formaldehyde, methanol, ethanol, alcohol blends and other hydrogen rich organics.
- the reductant is oxidized to produce protons, which migrate across the membrane to the cathode.
- the protons react with the oxidant.
- bipolar plates and the array of lands and grooves as “flow fields”.
- the flow field may be a separate porous electrode layer.
- Ideal separator plates for use in fuel cell stacks are thin, lightweight, durable, highly conductive, corrosion resistant structures that can also, if desired, provide effective flow fields and thereby become bipolar plates.
- the lands conduct current from the electrodes, while the grooves between the lands serve to distribute the gaseous reactants utilized by a fuel cell, such as hydrogen, oxygen or air, evenly over the faces of the electrodes.
- the channels formed by the lands and grooves also facilitate removal of liquid reaction byproducts, such as water.
- This thin sheet is normally termed a gas diffusion layer ("GDL"), and is incorporated as part of the MEA.
- Fuel cell stacks may also contain humidification channels within one or more of the coolant flow fields. These humidification channels provide a mechanism to humidify fuel and oxidants at a temperature as close as possible to the operating temperature of the fuel cell. This helps to prevent dehydration of the PEM as a high temperature differential between the gases entering the fuel cell and the temperature of the PEM causes water vapor to be transferred from the PEM to the fuel and oxidant streams.
- the location of the humidification channels can either be upstream from the MEA, such as in the fuel cell stacks described in U.S. Patent No. 5,382,478 to Chow et al, and U.S. Patent No. 6,066,408 to Nitale et al, or downstream from the MEA, such as those described in U.S. Patent No.
- Fuel cell stacks range in design depending upon power output, cooling, and other technical requirements, but may utilize a multitude of MEAs, seals, flow fields, and separator plates, in intricate assemblies that result in manufacturing difficulties and further increase fuel cell costs.
- one fuel cell stack described in U.S. Patent No. 5,683,828, to Spear et al., employs bipolar plates containing up to ten separate layers adhesively bonded together, each layer having distinct channels that are dedicated to passing cooling water through the fuel cell stack for thermal management.
- These multitudes of individual components are typically assembled into one sole complex unit to form the fuel cell stack.
- the stack is then compressed, generally through the use of end plates and bolts although banding or other methods may be used, such that the stack components are held tightly together to maintain electrical contact there between.
- These current means of applying compression add even more components and complexity to the stack and pose additional sealing requirements.
- Various attempts have been made in the fuel cell art to cure these deficiencies in fuel cell stack assembly design and thereby lower manufacturing costs.
- U.S. Patent No. 5,176,966, to Epp et al describes a method of forming at least some of the required gaskets directly into the fuel cell stack assembly. Specifically, the MEA is made with corresponding carbon paper and then an extrudable sealant is applied into grooves cut within the carbon paper.
- U.S. Patent No. 5,264,299, to Rrasij et al. describes a fuel cell module having a PEM interposed between the two porous support layers which distribute reactant to the catalyst layers in which the peripheral portion of the support layers are sealed with an elastomeric material such that the PEM is joined with the support layers and the open pores of the support layers are filled with the elastomeric material making it fluid impermeable.
- the elastomeric material solidifies to form a fluid impermeable frame for the PEM and support layer assembly.
- U.S. Patent No. 5,523,175, to Beal et al. describes an improvement of U.S. Patent No. 5,264,299 which comprises a plurality of gas distribution channels on the support layers and utilizes a hydrophilic material for sealing of the open pores.
- this improvement does not address the issue of gaps between the MEA and the support plates.
- Another object of the present invention provides a fuel cell stack comprised of pre- fabricated individual modules that are standardized to specific power outputs or other technical specifications thereby allowing for the quick and efficient assembly of a complete fuel cell stack with minimal manufacturing processes being employed, by combining such standardized modules to meet the required specifications of the completed fuel cell stack.
- Yet another object of the present invention is to provide for a reduction in the complexity of a fuel cell stack by reducing the number of components and seals required for stack construction, while maintaining the required power output for the stack, thereby increasing the reliability of the fuel cell stack.
- Still another object of the present invention is to provide for an improved method of sealing porous components within the stack or a module thereof, as well as a method of sealing the stack or module periphery that is less labor intensive and more suitable to high volume manufacturing processes.
- Still another object of the present invention is to provide a simplified compression means for the fuel cell stack assembly wherein the components of the fuel cell stack assembly would remain in close contact with a minimum of additional elements being added to the assembled stack.
- Each module referred to herein as a "fuel cell cassette” is a simplified stack assembly which has bonded internal manifolding and is externally encapsulated about its perimeter to form a self- contained unit.
- fuel cell cassettes may be designed to achieve standardized specifications and may be fabricated prior to the manufacture of the fuel cell stack.
- a fuel cell cassette comprises: a MEA having at least one MEA manifold opening extending through the thickness thereof wherein each of the membrane electrode assembly manifold openings is bonded at the perimeter by a first sealant; a fuel flow field having at least one fuel flow field manifold opening extending through the thickness thereof wherein each fuel flow field manifold opening which does not correspond to a manifold providing fuel reactant for distribution to the fuel flow field is bonded at the perimeter by a second sealant; an oxidant flow field having at least one oxidant flow field manifold opening extending through the thickness thereof wherein each oxidant flow field manifold opening which does not correspond to a manifold providing oxidant reactant for distribution to the oxidant flow field is bonded at the perimeter by a third sealant; wherein the MEA, the fuel flow field, and the oxidant flow field are assembled in a stack relative to each other such that the MEA manifold openings, the fuel flow field manifold openings, and the oxidant flow field manifold openings
- the number and arrangement of fuel cell components within an individual fuel cell cassette may vary according to the power output requirements or other technical specifications required for the finished cassette, and any of such components within the fuel cell cassette may be paired with a separator plate to separate the fuel/oxidant streams and to provide cassette stability.
- the fuel cell cassette may optionally include one or more coolant flow fields or humidification channels, if there were cooling requirements for the finished cassette or if a humidification section was desired.
- One or more fuel cell cassettes are then assembled together to form a complete fuel cell stack.
- V-ARTM vacuum assisted resin transfer molding
- a method of manufacturing a fuel cell cassette comprising the steps of: bonding at least one manifold opening which extends through the thickness of a MEA about the perimeter of the MEA manifold opening using a first sealant; bonding at least one manifold opening which extends through the thickness of a reactant flow field about the perimeter of the reactant flow field manifold opening using a second sealant, the reactant flow field having at least one reactant flow field manifold opening which is not bonded about the perimeter to allow for distribution of reactant into the reactant flow field; assembling the MEA and the reactant flow field relative to each other to form a stacked formation such that the reactant flow field manifold openings are aligned with the membrane electrode assembly manifold openings thereby defining at least one manifold channel which extends through the thickness of the stacked formation; stacking a non-porous layer adjacent to the top and bottom of the stacked formation to form a non-porous layer/stacked formation assemblage; applying a compression means to the non-porous
- assembly of the finished fuel cell stack is further simplified by interposing the fuel cell stack assembly between two joined housing pieces to apply compression to the components of the fuel cell stack without the addition of a multitude of end plates and bolts.
- the housing pieces are joined with a sealant.
- the fuel cell cassettes of the present invention may be used in fuel cell systems such as PEM fuel cells based on hydrogen or direct methanol and anion exchange membrane based alkaline fuel cells.
- the fuel cell cassettes of the present invention may also be used in a host of electrochemical applications that utilize electrolyte membranes other than the fuel cell systems discussed above. These applications include but are not limited to batteries, methanol/air cells, electrolyzers, concentrators, compressors and reactors. BRIEF DESCRIPTION OF THE DRAWINGS
- FIGURE 1A is a cross sectional view of one embodiment of a fuel cell cassette of the present invention.
- FIGURE IB is a top view of one embodiment of a fuel cell cassette of the present invention.
- FIGURE 2 is a cross sectional view of a second embodiment of the fuel cell cassette of the present invention.
- FIGURE 3 is a cross sectional view of a third embodiment of the fuel cell cassette of the present invention.
- FIGURE 4 is a cross sectional view of yet another embodiment of the fuel cell cassette of the present invention.
- FIGURE 5 is a top view of a MEA for use in the present invention wherein each manifold port has been bonded about its perimeter.
- FIGURE 6 is a cross sectional view of a port-seal fixture used in the manufacturing of the present invention which contains an assembly of MEAs and spacer films.
- FIGURE 7A is a cross sectional view of the edge encapsulation fixture used in the manufacturing of the present invention containing a fuel cell cassette assembly design.
- FIGURE 7B is a top view of the edge encapsulation fixture used in the manufacturing of the present invention containing a fuel cell cassette assembly design.
- FIGURE 8 is a cross sectional view of a fuel cell stack which is comprised of fuel cell cassettes of the present invention with the addition of end plates and a compression means.
- FIGURE 9 is cut away side view of a fuel cell stack encompassing three fuel cell cassettes of the present invention wherein the fuel cell cassettes are contained within two sealed housing pieces.
- a fuel cell cassette 1 of the present invention is shown.
- the fuel cell cassette 1 shown comprises two unit cells 7, each unit cell having a separator plate 6, a fuel flow field 3, a MEA 2, and an oxidant flow field 4.
- a coolant flow field 5 is sandwiched between the two unit cells 7, with the addition of separator plates 6, to provide cooling capability to the fuel cell cassette.
- the fuel cell cassette 1 is shown, in its present configuration to facilitate the illustration of the present invention.
- an individual fuel cell cassette may embody various assemblies of MEAs, flow field plates and separator plates, as well as other fuel cell components to form unit cells within the fuel cell cassette and also that each such unit cell may be repeated or combined with different unit cells, dependent upon the power output, humidification and/or cooling requirements for the completed fuel cell cassette.
- FIGURE 2 shows a fuel cell cassette 1 wherein the assembly for one unit cell 7 consists of (in this order): a separator plate 6, a fuel flow field 3, a MEA 2, and an oxidant flow field 4.
- bipolar fuel cell arrangement i FIGURE 2
- the bipolar fuel cell arrangement unit cell 7 is repeated more than once to illustrate that more than one unit cell 7 may be repeated, but unlike the assembly shown in FIGURE 1 A, no coolant flow field is employed.
- the unit cell 7 will normally be repeated more times than shown in FIGURE 2, since each additional unit cell 7 results in increased voltage output for the fuel cell cassette 1.
- FIGURE 3 shows a fuel cell cassette 1 having only one unit cell.
- a lower voltage fuel cell cassette 1 assembly may consist of only a fuel flow field 3, a MEA 2, and an oxidant flow field 4.
- FIGURE 4 shows another variation of a fuel cell cassette 1 assembly, which may be referred to as an "edge collection arrangement" (also known as a parallel or non-bipolar stack).
- a unit cell 8 consists of (in this order): a fuel flow field 3, a MEA 2, an oxidant flow field 4, and another MEA 2.
- Two edge collection arrangement unit cells 8 are shown in FIGURE 4, but as explained above, the unit cell 8 may be repeated as many times as necessary in the fuel cell cassette 1 to increase the current by the desired amount.
- FIGURE 4 shows an edge collection arrangement without a coolant flow field, however, a coolant flow field may be added by placing a separator plate, a coolant flow field, and another separator plate between any pair of fuel/oxidant flow fields.
- coolant flow fields may cool each unit cell, or none of them, depending upon the cassette design, hi still other fuel cell cassette designs, the reactant flow fields may be contained on a bipolar plate and not as separate layers. Any useful combination of the typical fuel cell component layers known to those skilled in the art may be used as the assembly for a fuel cell cassette of the present invention.
- the MEA 2 maybe purchased from commercial suppliers or otherwise maybe made in accordance with various methods of manufacturing known in the art, such as those methods described in U.S. Patent No. 5,330,860 to Grot et al; U.S. Patent No. 5,316,871 to Swathirajan et al, and U.S. Patent No. 5, 211,984 to Wilson.
- the anode side and cathode side, each on opposing faces of the membrane comprise either finely divided catalyst particles, such as platinum or its alloys, or finely divided carbon particles having the catalyst on its surfaces.
- the catalyst particles or catalyst-bearing carbon particles are dispersed throughout a polymeric binder or matrix that typically comprises either a proton conductive polymer and/or a fluoropolymer.
- the MEA 2 is constructed using a decal process wherein the catalyst ink is coated, painted, sprayed or screen-printed onto Teflon® or Kapton® blanks (both available commercially from E.I. duPont de Nemours and Company, U.S.A.), and the resulting decal is then transferred from the blank to the membrane surface and bonded, typically through the application of heat and pressure.
- a MEA 2 is fabricated wherein electrodes are coated with a catalyst containing a precious metal.
- finely distributed platinum is deposited onto specially treated carbon mats, at about 0.05 to about 10 milligrams of platinum per square centimeter, and a PEM is hot pressed between two such carbon mats with the coated side of the mats in contact with the membrane.
- PEMs useful in these MEAs include perfluorinated sulfonic acid membranes, such as National® (available commercially from E.I. duPont de Nemours and Company, U.S.A.), Gore-Select® (available commercially from W.L.
- the MEA 2 of the present invention includes one or more manifold openings 9 through its thickness of the MEA 2 to allow for fuel, oxidant and, if required, coolant access into the fuel cell cassette 1.
- manifold openings 9 maybe punch cut into the MEA 2 through the use of a die, laser cut into the MEA 2, or shaped by other suitable methods known in the art.
- the number and size of the openings 9 may vary and are dependent upon the design of the fuel cell cassette 1 and the shape and diameter of the access manifolds needed for the distribution of reactants and coolants into the fuel cell cassette. Generally, such manifold openings 9 are circular in shape, but the openings 9 may be formed in any geometric shape without limiting the usefulness of the methods described herein. In the preferred embodiment shown in FIGURE 1, the MEA 2 has a total of six circular manifold openings 9 - two for fuel access, two for oxidant access and two for coolant access. However, as mentioned above, those skilled in the art will recognize that the number and location of openings 9 is dependent upon the specific assembly design being utilized for the fuel cell cassette 1. For example, in the assembly shown in the assembly shown in the assembly shown in
- FIGURE 2 there is no coolant flow field. Therefore, no coolant access into the fuel cell cassette 1, and no manifold opening for such coolant access, is required.
- each manifold opening 9 of the MEA 2 is bonded about its perimeter by a sealant to enable gas and liquid distribution throughout the fuel cell cassette 1 to be controlled by the flow fields and to prevent leakage of the reactants from the manifold openings 9 into the MEA 2.
- FIGURE 5 shows a MEA 2 having each manifold opening bonded about its perimeter 10.
- the fuel flow field 3, the oxidant flow field 4, and the coolant flow field 5 may be purchased from commercial suppliers or otherwise may be made in accordance with various methods of manufacturing known in the art. In the preferred embodiment, laser cut stainless steel screens are employed for use as these fields.
- one or more of the flow fields are comprised of composite polymeric/graphite materials.
- Each flow field includes the same number of manifold openings 9 through its thickness as the number of manifold openings 9 included on the MEA 2. However, on each flow field 3, 4, and 5 the manifold openings 9 corresponding to the manifold openings 9 being utilized on that specific flow field plate for distribution of reactant or coolant remain unbonded while all other manifold openings 9 on such flow field are bonded about their perimeter 10.
- separator plate 6 should be thin, lightweight, durable, electrically conductive and corrosion resistant.
- stainless steel is used for the separator plate 6.
- graphite, titanium or any corrosion resistant alloy may also be used.
- one or more of the separator plates 6 could be fashioned from composite polymeric/graphite materials.
- Perimeter bonding 10 of specific manifold openings 9 of the porous components of the fuel cell cassette 1 is accomplished through the use of a pressure differential which allows the sealant to be drawn into and impregnated within the interstices of the porous component surrounding the manifold opening 9.
- the pressure differential is accomplished by vacuum assisted resin transfer molding.
- the porous components include the GDL of the MEA 2 and the fuel, oxidant and coolant flow fields 3, 4 and 5, but the separator plates 6 are non-porous and do not require bonding about the perimeter of any manifold openings.
- Other fuel cell cassette designs known to those skilled in the art may include other porous components which may also be bonded through the use of the process described herein.
- the vacuum assisted resin transfer molding process for such perimeter bonding 10 is accomplished by first cutting a non-porous polymeric spacer film 16 with the same manifold opening configuration as the MEA 2. If more than one MEA 2 is being bonded at one time, then the MEAs 2 and spacer films 16 are stacked, one on top of the other, with the manifold openings 9 of the MEAs 2 and the spacer films 16 aligned to form a MEA/spacer film assembly 11. The MEA/spacer film assembly 11 is then placed into a port-seal-fixture ("PSF") 12 as shown in FIGURE 6.
- PSF port-seal-fixture
- the port-seal-fixture 12 consists of a mold 13, top seal/compression plate 14, bolts 15 and vacuum holes 27.
- the number and location of manifold openings in each MEA component are as shown in FIGURE IB such that six manifold channels 29 are formed in the MEA/spacer film assembly.
- Bolts 15 are then placed through the four corner manifold channels 29 of the MEA/spacer film assembly 11 to act as a compression means and also to seal the MEA/spacer film assembly 11 against any sealant flow in the direction perpendicular to the surface of the MEAs 2.
- any compression means which is capable of uniformly distributing the load over the entire surface of the MEA/spacer film assembly 11 may be employed as the compression means, including external press, bolting, or banding.
- a free-flowing resin is introduced into the entire volume of each opening 9.
- the vacuum holes 27 are used, with the appropriate fittings, to pull a vacuum on the MEA spacer film assembly 11 for a preset time such that the resin is drawn into each MEA 2 of the MEA/spacer film assembly 11 and is impregnated within each MEA 2 at the perimeter of the manifold openings 9 being bonded.
- the vacuum is confined to the edges of the MEA/spacer film assembly 11 by adding an additional non-porous polymer spacer film 16 layer on the top and bottom of the assembly 11 in combination with an O-ring gasket seal 26 in the top compression plate 14 as a sealing means.
- the sealant utilized to bond the perimeter of the manifold openings 9 is selected such that it is free-flowing and fills the void spaces.
- the sealant must also be chosen with regard to the chemical and mechanical properties required for the conditions encountered in an operating fuel cell system. For example, the sealant must be non-reactive with the reactants and byproducts within the fuel cell system and must be able withstand the operating temperature of the fuel cell system. Further, the sealant must not shrink or release more than minimal amounts of solvent into the fuel cell system. Sealants useful in the present invention include both thermoplastics and thermoset elastomers.
- thermoplastic sealants include, but are not limited to, thermoplastic olefin elastomers, such as Santoprene® (available commercially from Advanced Elastomer Systems, L.P., U.S.A.), thermoplastic polyurethanes or plastomers, such as Exact® (available commercially from The Exxon Corporation, U.S.A.), polypropylene, polyethylene, polytetrafluoroethylene, fluorinated polypropylene, and polystyrene.
- thermoplastic olefin elastomers such as Santoprene® (available commercially from Advanced Elastomer Systems, L.P., U.S.A.)
- thermoplastic polyurethanes or plastomers such as Exact® (available commercially from The Exxon Corporation, U.S.A.)
- Exact® available commercially from The Exxon Corporation, U.S.A.
- polypropylene polyethylene
- polytetrafluoroethylene fluorinated polyprop
- thermoset elastomer sealants include, but are not limited to, epoxy resins, such as 9223-2 (available commercially from the Minnesota Mining and Manufacturing Company, U.S.A.) and AY105/HY991 (available commercially from Ciba Specialty Chemical Corporation, U.S.A.), PUR resin such as Araldite®2018 (available commercially from Ciba Specialty Chemical Corporation, U.S.A), ALIPS resin such as FEC2234 (available commercially from Morton International, Inc., U.S.A.), SYLGARD® 170 A/B (available commercially from Dow Corning Corporation, U.S.A.), Fluorel® resin (available commercially from the Minnesota Mining and Manufacturing Company, U.S.A.), Fluorolast® resin (available commercially from Lauren International, Inc, U.S.A.), urethanes, silicones, fluorosilicones, and vinyl esters.
- epoxy resins such as 9223-2 (available commercially from the Minnesota Mining and Manufacturing Company, U.S
- manifold openings 9 must also be bonded on the various porous components to be utilized in the fuel cell cassette 1, such as the flow fields 3, 4, and 5, in order to control gas and liquid distributed throughout the fuel cell cassette 1.
- the MEA 2 requires all manifold openings 9 to be bonded 10 as distribution of fuel/oxidant into the stack occurs through the reactant flow fields 3 and 4.
- each flow field 3, 4, and 5 requires distribution of a reactant or coolant into the flow field, and it is desirable to prevent leakage of such reactant or coolant to the incorrect flow field.
- the manifold openings 9 from which oxygen (pure or in air) will enter the fuel cell cassette 1 must remain open to allow for diffusion of the oxidant across the MEA 2.
- These porous components may have additional manifold openings 9 to allow for manifold access through the fuel cell cassette 1 for distribution to other flow fields and these remaining manifold openings 9 must be bonded to prevent the diffusion of gas or coolant into the incorrect flow field. Therefore, each flow field 3, 4, and 5 will have different positioning of bonded and unbonded manifold openings 9.
- the final fuel cell cassette 1 design assembly consists of the following components (in the following order): a separator plate 6, a fuel flow field 3, a MEA 2, and oxidant flow field 4, a separator plate 6, a coolant flow field 5, a separator plate 6, a fuel flow field 3, a MEA 2, an oxidant flow field 4, and a separator plate 6.
- the final fuel cell cassette design assembly is formed such that all components are assembled relative to each other to form a stacked formation having the manifold openings 9 located on each component aligned with the mamfold openings 9 located on the other components to define a plurality of manifold channels 29 extending through the thickness of the fuel cell cassette assembly. If other assembly designs are utilized, such as those shown in FIGURE 2 and FIGURE 3, the components would be aligned in the same manner.
- Each of the components of the fuel cell cassette design assembly is bonded along its peripheral edges 18 with the other components in the fuel cell cassette design assembly in order to form the completed fuel cell cassette 1 of the present invention, such that the fuel cell cassette 1 has a fully encapsulated edge periphery 18 to separate the fuel cell cassette components from the outside environment thereby preventing membrane dry out on exposure to the ambient and to provide structural support for the fuel cell cassette 1.
- the peripheral edge encapsulation is conducted through the use of a pressure differential which draws the resin into the interstices of any porous components and within the spaces separating one component from the other and impregnates the resin there between, hi one preferred embodiment, the pressure differential is accomplished through vacuum assisted resin transfer molding.
- a piece of non-porous polymeric spacer 16 film is placed on both the top and bottom sides of the final design assembly for the fuel cell cassette 1 in order to cap the assembly.
- the cassette/film assembly 20 is then placed into the edge encapsulation fixture ("EEF") 19, as shown in FIGURE 7A and FIGURE 7B.
- the EEF 19 consists of a mold 30, top seal/vacuum plate 21, vacuum fittings 31 to the manifold channels 29 and a compression means.
- the top seal/vacuum plate 21 serves two functions: It evenly distributes the load to the cassette/film assembly 20 and contains fittings 31 to uniformly introduce vacuum to each manifold channel 29.
- the compression means is required to insure that the flowable resin fully encapsulates the non-porous components while using the minimum amount of resin 17. There must be enough compliance in the cassette/film assembly 20 to uniformly distribute the load over its entire surface.
- a number of techniques can be used to supply the required load and compression means, including an external press, bolting, or banding.
- a guide mechanism is used to ensure that the top seal/vacuum plate 21 remains perpendicular to the base ofthe EEF 19.
- a compressive load is first applied to the cassette/film assembly 20 using torque bolts 15 or a hand press.
- a free- flowing resin 17 is poured into the mold 30, outside the periphery of the cassette/film assembly 20. Any resin 17 useful for the perimeter bonding of the manifold openings 9 of the porous components may be used for the encapsulation of the periphery of the fuel cell cassette 1.
- a vacuum is applied to the EEF 19 through the vacuum fittings 31.
- the compressive load insures that the vacuum is pulled only in the manifold openings 9 via the manifold channels 29.
- the resin 17 flows into the outer edges of the fuel cell cassette/film assembly 20, thereby encapsulating the peripheral edges of the porous and non- porous components of the fuel cell cassette 1.
- This provides a secondary seal for all flow fields and other porous components by separating the entire fuel cell cassette 1 periphery from the outside environment while also preventing the edges of all such porous components from drying out on exposure to the ambient environment.
- the encapsulated periphery 18 provides structural support for the fuel cell cassette 1 and a surface area on the resulting fuel cell cassette 1 on which the fittings and other hardware needed for reactant, coolant, and current distribution can be fixed.
- the resin 17 is allowed to sit within the mold 30 of the EEF 19 and solidify. Once hardening is complete, the top seal/vacuum plate 21 is removed, followed by the removal of the non-porous film 16 layer from each side of the fuel cell cassette 1. The top and bottom edge of the fuel cell cassette 1 may then be trimmed and the edges routed to remove any excess resin.
- FIGURE 8 a fuel cell stack 22 comprising two fuel cell cassettes 1 of the present invention is shown, hi such fuel cell stack 22, endplates 23 and further compression means, such as bolts 15, have been added to secure the fuel cell stack 22.
- the endplates 23 are heavy metallic structures, with internal channels for the flow of reactants and coolant, as well as bolts and gaskets for compression. A number of endplate configurations are known to those skilled in the art. Electrical contacts 28 are also provided to remove the electrical energy produced by the working fuel cell stack.
- FIGURE 8 shows a fuel cell stack 22 comprising two fuel cell cassettes 1
- any other number of fuel cell cassettes 1 may be utilized in the fuel cell stack 22 depending upon final output requirements of the fuel cell system. If lower output requirements are sufficient, a fuel cell stack may consist of only one fuel cell cassette with the addition of endplates or other compression means. If more than one fuel cell cassette 1 is utilized for the fuel cell stack, such as in FIGURE 8, each fuel cell cassette must be stacked such that the manifold openings of all the fuel cell cassettes 1 are aligned to form manifold channels 29 extending through the fuel cell stack 22.
- a fuel cell stack 22 may be manufactured in which the fuel cell cassettes 1 of the present invention are contained within two housing pieces 24 as shown in FIGURE 9.
- the housing pieces 24 may be formed of metal, thermosets, or traditional engineering thermoplastics.
- Preferred thermoplastics include polyether sulfones, polyphenylene sulfones, polyphenylene sulfide, polysulfone, polyphenylene oxide, polyphenylene ether, polypropylene, polyethylene, polytetrafluoroethylene, and fluorinated polypropylene, or blends thereof.
- thermoplastic material may contain a filler material, such as glass fibers, graphite fibers, aramid fibers, ceramic fibers, silica, talc, calcium carbonate, silicon carbide, graphite powder, boron nitride, polytetrafluoroethylene, and metal powders or fibers, h one preferred embodiment, the housing pieces are formed from a glass fiber filled polysulfone.
- Preferred thermosets include epoxies or polyurethanes.
- a fuel cell stack 22 which comprises a first housing piece 24 having a base opening and a sidewall opening extending from the base opening to define a first storage compartment and having at least one reactant manifold opening 9 extending through the thickness of the base opening.
- a second housing piece 24 is shown having a top opening and a sidewall opening extending from the top opening to define a second storage compartment and further having at least one reactant manifold opening 9 extending through the thickness of the top opening.
- One or more fuel cell cassettes 1 of the present invention are placed within the storage compartment of the base portion of the first housing piece 24.
- FIGURE 9 there are three such fuel cell cassettes 1 being utilized for the fuel cell stack 22. If more than one fuel cell cassette 1 is stacked, the fuel cassettes 1 must be stacked such that the manifold openings 9 of all the fuel cell cassettes 1 are aligned. The top portion of the second housing piece 24 may then be placed such that the sidewall portion of the second housing piece 24 is resting on the sidewall portion of the first housing piece 24.
- both first and second housing pieces 24 contain manifold openings 9, such as shown in FIGURE 9, then the reactant manifold openings 9 of the first housing piece 24 are aligned with the manifold openings 9 of the second housing piece 24 and the manifold openings 9 of the fuel cell cassettes 1 to form manifold channels 29 through the thickness of the fuel cell stack 22 and both housing pieces 24.
- only one of the housing pieces 24 may contain manifold openings 9 and the manifold channels 29 may only extend through the fuel cell cassettes 1 and one of the housing pieces 24.
- the two housing pieces 24 may be joined, preferably by means of a sealant 25, although bolts or other mechanical means of joining may be used.
- sealing is accomplished by first applying a compression means to the two housing pieces 24.
- the compression means may be a platen press, fasteners or other compression means known in the art.
- a sealant 25 is then injected by an injection molding process at the interface of the sidewall portions of the first and second housing pieces 24.
- the sealant 25 is selected with regard to the chemical and mechanical properties required for the conditions encountered in an operating fuel cell system, such as the ability to withstand the operating temperatures within such fuel cell system.
- the sealant 25 is polypropylene, but other polymer sealants known in the art, such as urethanes or epoxies may also be used.
- Sealants which may be used also include, but are not limited to, PUR resin such as Araldite®2018 (available commercially from Ciba Specialty Chemical Corporation, U.S.A.), ALIPS resin such as FEC2234 (available commercially from Morton International, hie, U.S.A.), SYLGARD® 170 A/B (available commercially from Dow Corning Corporation, U.S.A.), Fluorel® resin (available commercially from the Minnesota Mining and Manufacturing Company, U.S.A.), Fluorolast® resin (available commercially from Lauren International, h e, U.S.A.), silicones, fluorosilicones, and vinyl esters.
- PUR resin such as Araldite®2018 (available commercially from Ciba Specialty Chemical Corporation, U.S.A.)
- ALIPS resin such as FEC2234 (available commercially from Morton International, hie, U.S.A.), SYLGARD® 170 A/B (available commercially from Dow Corning Corporation, U.S
- a fuel cell stack 22 formation comprised of fuel cell cassettes 1 of the present invention is thereby encased within the storage compartments of the two joined housing pieces 24 while reactant access to the fuel cell stack 22 is provided through the manifold channels 29 through manifold connectors 32. While preferred embodiments have been shown and described, various modifications and substitutions may be made without departing from the spirit and scope of the invention. Accordingly, it is to be understood that the present invention has been described by way of example, and not by limitation.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Fuel Cell (AREA)
- Conductive Materials (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Secondary Cells (AREA)
- Electric Double-Layer Capacitors Or The Like (AREA)
Abstract
Description
Claims
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2002217974A AU2002217974A1 (en) | 2000-11-27 | 2001-11-27 | Electrochemical polymer electrolyte membrane cell stacks |
JP2002544801A JP4346905B2 (en) | 2000-11-27 | 2001-11-27 | Electrochemical polymer electrolyte membrane battery stack |
CA2430083A CA2430083C (en) | 2000-11-27 | 2001-11-27 | Electrochemical polymer electrolyte membrane cell stacks |
DE60138045T DE60138045D1 (en) | 2000-11-27 | 2001-11-27 | ELECTROCHEMICAL POLYMER ELECTROLYTEMEMBRANZELLSTAPEL |
EP01997859A EP1356532B1 (en) | 2000-11-27 | 2001-11-27 | Electrochemical polymer electrolyte membrane cell stacks |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US25319900P | 2000-11-27 | 2000-11-27 | |
US60/253,199 | 2000-11-27 | ||
US09/908,359 | 2001-07-18 | ||
US09/908,359 US6946210B2 (en) | 2000-11-27 | 2001-07-18 | Electrochemical polymer electrolyte membrane cell stacks and manufacturing methods thereof |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2002043173A1 true WO2002043173A1 (en) | 2002-05-30 |
Family
ID=26943016
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2001/044880 WO2002043173A1 (en) | 2000-11-27 | 2001-11-27 | Electrochemical polymer electrolyte membrane cell stacks |
Country Status (8)
Country | Link |
---|---|
US (2) | US6946210B2 (en) |
EP (1) | EP1356532B1 (en) |
JP (1) | JP4346905B2 (en) |
AT (1) | ATE426252T1 (en) |
AU (1) | AU2002217974A1 (en) |
CA (1) | CA2430083C (en) |
DE (1) | DE60138045D1 (en) |
WO (1) | WO2002043173A1 (en) |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6805990B2 (en) * | 2001-10-24 | 2004-10-19 | Fuelcell Energy, Ltd. | Flat plate fuel cell stack |
US6852439B2 (en) | 2001-05-15 | 2005-02-08 | Hydrogenics Corporation | Apparatus for and method of forming seals in fuel cells and fuel cell stacks |
WO2004051766A3 (en) * | 2002-12-04 | 2005-03-10 | Lynntech Power Systems Ltd | Adhesively bonded electrochemical cell stacks |
US7052796B2 (en) | 2003-02-27 | 2006-05-30 | Protonex Technology Corporation | Externally manifolded membrane based electrochemical cell stacks |
US7306864B2 (en) | 2001-10-22 | 2007-12-11 | Protonex Technology Corporation | One-shot fabrication of membrane-based electrochemical cell stacks |
EP1836738A4 (en) * | 2004-12-29 | 2009-04-29 | Utc Power Corp | Fuel cell separator plate assembly |
US7687181B2 (en) | 2002-04-23 | 2010-03-30 | Protonex Technology Corporation | Channel-based electrochemical cassettes |
US7695846B2 (en) | 2002-11-18 | 2010-04-13 | Protonex Technology Corporation | Membrane based electrochemical cell stacks |
US7879507B2 (en) | 2006-04-10 | 2011-02-01 | Protonex Technology Corporation | Insert-molded, externally manifolded, one-shot sealed membrane based electrochemical cell stacks |
US8124292B2 (en) | 2007-06-28 | 2012-02-28 | Protonex Technology Corporation | Fuel cell stacks and methods |
US8580457B2 (en) | 2007-06-28 | 2013-11-12 | Protonex Technology Corporation | Fuel cell stack sealed with encapsulating material and method of making the same |
US8758958B2 (en) | 2004-12-29 | 2014-06-24 | Clearedge Power, Llc | Fuel cell separator plate assembly |
DE102018101316A1 (en) | 2017-01-23 | 2018-07-26 | GM Global Technology Operations LLC | MICRICUTTURE FOR FUEL CELLS AND METHOD FOR MANUFACTURING THE SAME |
Families Citing this family (39)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6946210B2 (en) * | 2000-11-27 | 2005-09-20 | Protonex Technology Corporation | Electrochemical polymer electrolyte membrane cell stacks and manufacturing methods thereof |
US20050095492A1 (en) * | 2001-05-15 | 2005-05-05 | Hydrogenics Corporation | Fuel cell stack |
US6821666B2 (en) * | 2001-09-28 | 2004-11-23 | The Regents Of The Univerosity Of California | Method of forming a package for mems-based fuel cell |
DE10160905B4 (en) * | 2001-12-12 | 2007-07-19 | Carl Freudenberg Kg | Sealing arrangement for fuel cells, method for producing and using such a sealing arrangement |
WO2004027896A2 (en) * | 2002-09-23 | 2004-04-01 | Protonex Technology Corporation | Liquid electrochemical cell stacks and manufacturing methods for same |
JP4067371B2 (en) | 2002-09-25 | 2008-03-26 | 本田技研工業株式会社 | Fuel cell |
US20050048349A1 (en) * | 2003-08-28 | 2005-03-03 | Fannon Megan A. | Method of manufacturing a fuel cell array and a related array |
US7297269B2 (en) * | 2003-10-31 | 2007-11-20 | Protonex Technology Corporation | Cross-flow filtration cassettes and methods for fabrication of same |
US20070212587A1 (en) * | 2005-04-01 | 2007-09-13 | Nick Fragiadakis | Apparatus for and method of forming seals in an electrochemical cell assembly |
NO20053220D0 (en) * | 2005-06-29 | 2005-06-29 | Norsk Hydro As | Compression of a PEM cell stack in a pressure tank. |
US7914943B2 (en) * | 2005-08-19 | 2011-03-29 | Daimler Ag | Integrated seal for fuel cell assembly and fuel cell stack |
US20070048580A1 (en) * | 2005-08-30 | 2007-03-01 | Cheng-Hsin Chen | Fuel cell |
DE502005004821D1 (en) * | 2005-09-06 | 2008-09-04 | Sgl Carbon Ag | Electrodes for fuel cells |
EP2266682A3 (en) * | 2005-09-09 | 2014-08-20 | Tangenx Technology Corporation | Laminated cassette device and method for making same |
FR2891950B1 (en) * | 2005-10-11 | 2014-05-30 | Commissariat Energie Atomique | FUEL CELL SEALED STACK |
WO2007075862A2 (en) * | 2005-12-20 | 2007-07-05 | Tangenx Technology Corporation | Filtration assembly and methods for making and using same |
KR100821033B1 (en) | 2007-04-12 | 2008-04-08 | 삼성에스디아이 주식회사 | Fuel cell stack and manufacturing method |
US20090123784A1 (en) * | 2007-09-13 | 2009-05-14 | Pavlik Thomas J | Fuel cell module |
KR101274893B1 (en) * | 2008-08-05 | 2013-06-14 | 주식회사 엘지화학 | Stack and folding-typed electrode assembly and electrochemical cell comprising the Same |
US8236067B2 (en) * | 2008-08-11 | 2012-08-07 | GM Global Technology Operations LLC | Method and apparatus for fuel cell stack assembly |
US20110171562A1 (en) * | 2010-01-08 | 2011-07-14 | Gm Global Technology Operations, Inc. | Process for forming a membrane-subgasket assembly using vacuum sealing |
US20110229790A1 (en) * | 2010-03-19 | 2011-09-22 | Kenji Sato | Fuel cell module and fuel cell stack |
CN101826620B (en) * | 2010-03-30 | 2014-08-13 | 上海恒劲动力科技有限公司 | Bipolar plate for fuel cells |
KR20120105331A (en) * | 2011-03-15 | 2012-09-25 | 현대자동차주식회사 | Fuel cell stack with improved corrosion-resistance |
JP2013004352A (en) * | 2011-06-17 | 2013-01-07 | Toyota Motor Corp | Fuel cell system |
CN103915631B (en) * | 2012-12-31 | 2018-04-24 | 上海恒劲动力科技有限公司 | A kind of air-cooled integrated bipolar plates of fuel cell |
US10096844B2 (en) | 2013-10-03 | 2018-10-09 | Hamilton Sundstrand Corporation | Manifold for plural fuel cell stacks |
WO2017197406A1 (en) | 2016-05-13 | 2017-11-16 | Quantumscape Corporation | Solid electrolyte separator bonding agent |
DE102016221998A1 (en) * | 2016-11-09 | 2018-05-09 | Bayerische Motoren Werke Aktiengesellschaft | Method for producing a fuel cell stack |
EP3589587B1 (en) * | 2017-03-01 | 2023-08-09 | Axine Water Technologies Inc. | Electrochemical cell and stack of electrochemical cells for wastewater treatment with isolated electrodes |
CN111418086B (en) * | 2017-11-28 | 2023-11-24 | 昆腾斯科普电池公司 | Catholyte management for solid state separators |
WO2019143771A1 (en) * | 2018-01-17 | 2019-07-25 | Nuvera Fuel Cells, LLC | Electrochemical cells with improved fluid flow design |
JP7465217B2 (en) | 2018-06-06 | 2024-04-10 | クアンタムスケープ バッテリー,インコーポレイテッド | All-solid-state battery |
IL259978B (en) * | 2018-06-12 | 2020-07-30 | Pocell Tech Ltd | Alkaline membrane fuel cell assembly comprising a thin membrane and method of making same |
DE102018212715A1 (en) * | 2018-07-31 | 2020-02-06 | Robert Bosch Gmbh | Fuel cell stack and method for producing a fuel cell stack |
DE102018213912A1 (en) * | 2018-08-17 | 2020-02-20 | Audi Ag | Fuel cell device and method for monitoring and structural adaptation of a fuel cell device |
FR3102308B1 (en) * | 2019-10-18 | 2022-06-03 | Air Liquide | Fuel cell bipolar plate |
KR20210049339A (en) * | 2019-10-25 | 2021-05-06 | 현대자동차주식회사 | Fuel cell |
MX2024003095A (en) | 2021-09-27 | 2024-04-05 | Quantumscape Battery Inc | Electrochemical stack and method of assembly thereof. |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0122150A2 (en) * | 1983-04-11 | 1984-10-17 | Engelhard Corporation | Integral gas seal for fuel cell gas distribution assemblies and method of fabrication |
US5110691A (en) * | 1991-01-16 | 1992-05-05 | International Fuel Cells Corporation | Fuel cell component sealant |
US5176966A (en) * | 1990-11-19 | 1993-01-05 | Ballard Power Systems Inc. | Fuel cell membrane electrode and seal assembly |
US5453331A (en) * | 1994-08-12 | 1995-09-26 | University Of Chicago | Compliant sealants for solid oxide fuel cells and other ceramics |
US6159628A (en) * | 1998-10-21 | 2000-12-12 | International Fuel Cells Llc | Use of thermoplastic films to create seals and bond PEM cell components |
Family Cites Families (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1902392C3 (en) | 1969-01-18 | 1975-07-03 | Siemens Ag, 1000 Berlin Und 8000 Muenchen | Process for the production of fuel elements cast with plastic |
US4397917A (en) | 1982-01-11 | 1983-08-09 | Energy Research Corporation | Fuel cell pack with internal connection of fuel cells |
US4604331A (en) | 1984-05-29 | 1986-08-05 | The United States Of America As Represented By The United States Department Of Energy | Fuel cell separator plate with bellows-type sealing flanges |
JPH0260063A (en) * | 1988-08-24 | 1990-02-28 | Meidensha Corp | Stacked fuel cell |
US5264299A (en) | 1991-12-26 | 1993-11-23 | International Fuel Cells Corporation | Proton exchange membrane fuel cell support plate and an assembly including the same |
WO1993013566A1 (en) | 1991-12-26 | 1993-07-08 | International Fuel Cells, Inc. | Plate-shaped fuel cell component and a method of making the same |
JP4037448B2 (en) * | 1995-05-25 | 2008-01-23 | 本田技研工業株式会社 | Fuel cell |
DE19703214C2 (en) * | 1997-01-29 | 2003-10-30 | Proton Motor Fuel Cell Gmbh | Membrane electrode unit with integrated sealing edge and process for its manufacture |
US5858569A (en) * | 1997-03-21 | 1999-01-12 | Plug Power L.L.C. | Low cost fuel cell stack design |
DE19713250C2 (en) | 1997-03-29 | 2002-04-18 | Ballard Power Systems | Electrochemical energy converter with polymer electrolyte membrane |
DE69818874T2 (en) * | 1997-07-16 | 2004-05-19 | Ballard Power Systems Inc., Burnaby | Process for producing an elastic seal for the membrane electrode arrangement (mea) in an electrochemical fuel cell |
CN1122322C (en) * | 1998-04-17 | 2003-09-24 | 松下电器产业株式会社 | Solid polymer electrolyte fuel cell and method for producing the same |
US6165634A (en) | 1998-10-21 | 2000-12-26 | International Fuel Cells Llc | Fuel cell with improved sealing between individual membrane assemblies and plate assemblies |
US6399234B2 (en) | 1998-12-23 | 2002-06-04 | Utc Fuel Cells, Llc | Fuel cell stack assembly with edge seal |
US6372372B1 (en) * | 2000-02-11 | 2002-04-16 | Plug Power Inc. | Clamping system for a fuel cell stack |
US6596427B1 (en) * | 2000-11-06 | 2003-07-22 | Ballard Power Systems Inc. | Encapsulating seals for electrochemical cell stacks and methods of sealing electrochemical cell stacks |
US6946210B2 (en) * | 2000-11-27 | 2005-09-20 | Protonex Technology Corporation | Electrochemical polymer electrolyte membrane cell stacks and manufacturing methods thereof |
US6852439B2 (en) | 2001-05-15 | 2005-02-08 | Hydrogenics Corporation | Apparatus for and method of forming seals in fuel cells and fuel cell stacks |
US20020172852A1 (en) | 2001-05-15 | 2002-11-21 | David Frank | Flow field plate for a fuel cell and fuel cell assembly incorporating the flow field plate |
WO2003036747A1 (en) * | 2001-10-22 | 2003-05-01 | Protonex Technology Corporation | One-shot fabrication of membrane-based electrochemical cell stacks |
-
2001
- 2001-07-18 US US09/908,359 patent/US6946210B2/en not_active Expired - Lifetime
- 2001-11-27 AT AT01997859T patent/ATE426252T1/en not_active IP Right Cessation
- 2001-11-27 WO PCT/US2001/044880 patent/WO2002043173A1/en active Application Filing
- 2001-11-27 EP EP01997859A patent/EP1356532B1/en not_active Expired - Lifetime
- 2001-11-27 CA CA2430083A patent/CA2430083C/en not_active Expired - Lifetime
- 2001-11-27 DE DE60138045T patent/DE60138045D1/en not_active Expired - Lifetime
- 2001-11-27 AU AU2002217974A patent/AU2002217974A1/en not_active Abandoned
- 2001-11-27 JP JP2002544801A patent/JP4346905B2/en not_active Expired - Lifetime
-
2005
- 2005-09-16 US US11/229,087 patent/US7482086B2/en not_active Expired - Lifetime
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0122150A2 (en) * | 1983-04-11 | 1984-10-17 | Engelhard Corporation | Integral gas seal for fuel cell gas distribution assemblies and method of fabrication |
US5176966A (en) * | 1990-11-19 | 1993-01-05 | Ballard Power Systems Inc. | Fuel cell membrane electrode and seal assembly |
US5110691A (en) * | 1991-01-16 | 1992-05-05 | International Fuel Cells Corporation | Fuel cell component sealant |
US5453331A (en) * | 1994-08-12 | 1995-09-26 | University Of Chicago | Compliant sealants for solid oxide fuel cells and other ceramics |
US6159628A (en) * | 1998-10-21 | 2000-12-12 | International Fuel Cells Llc | Use of thermoplastic films to create seals and bond PEM cell components |
Cited By (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6852439B2 (en) | 2001-05-15 | 2005-02-08 | Hydrogenics Corporation | Apparatus for and method of forming seals in fuel cells and fuel cell stacks |
US7138202B2 (en) | 2001-05-15 | 2006-11-21 | Hydrogenics Corporation | Apparatus for and method of forming seals in fuel cells and fuel stacks |
US7210220B2 (en) | 2001-05-15 | 2007-05-01 | Hydrogenics Corporation | Apparatus for and method of forming seals in fuel cells and fuel stacks |
US7348092B2 (en) | 2001-05-15 | 2008-03-25 | Hydrogenics Corporation | Apparatus for and method of forming seals in fuel cells and fuel stacks |
EP1446851A4 (en) * | 2001-10-22 | 2008-11-19 | Protonex Technology Corp | One-shot fabrication of membrane-based electrochemical cell stacks |
US8232015B2 (en) | 2001-10-22 | 2012-07-31 | Protonex Technology Corporation | One-shot fabrication of membrane based electrochemical cell stacks |
US7306864B2 (en) | 2001-10-22 | 2007-12-11 | Protonex Technology Corporation | One-shot fabrication of membrane-based electrochemical cell stacks |
US6805990B2 (en) * | 2001-10-24 | 2004-10-19 | Fuelcell Energy, Ltd. | Flat plate fuel cell stack |
US7687181B2 (en) | 2002-04-23 | 2010-03-30 | Protonex Technology Corporation | Channel-based electrochemical cassettes |
US7695846B2 (en) | 2002-11-18 | 2010-04-13 | Protonex Technology Corporation | Membrane based electrochemical cell stacks |
WO2004051766A3 (en) * | 2002-12-04 | 2005-03-10 | Lynntech Power Systems Ltd | Adhesively bonded electrochemical cell stacks |
US7052796B2 (en) | 2003-02-27 | 2006-05-30 | Protonex Technology Corporation | Externally manifolded membrane based electrochemical cell stacks |
EP1836738A4 (en) * | 2004-12-29 | 2009-04-29 | Utc Power Corp | Fuel cell separator plate assembly |
US8758958B2 (en) | 2004-12-29 | 2014-06-24 | Clearedge Power, Llc | Fuel cell separator plate assembly |
US7879507B2 (en) | 2006-04-10 | 2011-02-01 | Protonex Technology Corporation | Insert-molded, externally manifolded, one-shot sealed membrane based electrochemical cell stacks |
US7887974B2 (en) | 2006-04-10 | 2011-02-15 | Protonex Technology Corporation | Insert-molded, externally manifolded, sealed membrane based electrochemical cell stacks |
US7914947B2 (en) | 2006-04-10 | 2011-03-29 | Protonex Technology Corporation | Insert-molded, externally manifolded, sealed membrane based electrochemical cell stacks |
US8124292B2 (en) | 2007-06-28 | 2012-02-28 | Protonex Technology Corporation | Fuel cell stacks and methods |
US8580457B2 (en) | 2007-06-28 | 2013-11-12 | Protonex Technology Corporation | Fuel cell stack sealed with encapsulating material and method of making the same |
DE102018101316A1 (en) | 2017-01-23 | 2018-07-26 | GM Global Technology Operations LLC | MICRICUTTURE FOR FUEL CELLS AND METHOD FOR MANUFACTURING THE SAME |
Also Published As
Publication number | Publication date |
---|---|
DE60138045D1 (en) | 2009-04-30 |
US6946210B2 (en) | 2005-09-20 |
US20060024545A1 (en) | 2006-02-02 |
JP4346905B2 (en) | 2009-10-21 |
EP1356532A4 (en) | 2007-02-21 |
EP1356532B1 (en) | 2009-03-18 |
CA2430083A1 (en) | 2002-05-30 |
EP1356532A1 (en) | 2003-10-29 |
AU2002217974A1 (en) | 2002-06-03 |
US7482086B2 (en) | 2009-01-27 |
CA2430083C (en) | 2010-11-09 |
ATE426252T1 (en) | 2009-04-15 |
JP2004534350A (en) | 2004-11-11 |
US20020068212A1 (en) | 2002-06-06 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP1356532B1 (en) | Electrochemical polymer electrolyte membrane cell stacks | |
CA2506592C (en) | Membrane electrode assembly with periphery gasket and sealing channels | |
US8232015B2 (en) | One-shot fabrication of membrane based electrochemical cell stacks | |
AU2005299831B8 (en) | Membrane based electrochemical cell stacks | |
CA2516765C (en) | Externally manifolded membrane based electrochemical cell stacks | |
US7879507B2 (en) | Insert-molded, externally manifolded, one-shot sealed membrane based electrochemical cell stacks | |
EP1502313B1 (en) | Membrane based electrochemical cell stacks | |
AU2003295710B2 (en) | Membrane based electrochemical cell stacks | |
AU2002363067A1 (en) | One-shot fabrication of membrane-based electrochemical cell stacks |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ PL PT RO RU SD SE SG SI SK SL TJ TM TR TT TZ UA UG UZ VN YU ZA ZW |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
WWE | Wipo information: entry into national phase |
Ref document number: 2002544801 Country of ref document: JP Ref document number: 2430083 Country of ref document: CA |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2001997859 Country of ref document: EP |
|
REG | Reference to national code |
Ref country code: DE Ref legal event code: 8642 |
|
WWP | Wipo information: published in national office |
Ref document number: 2001997859 Country of ref document: EP |